Electrochemical Cell Electrode Catalytic Activity Distribution

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Solution Overview

Problem

Existing electrochemical cells face issues with spatial nonuniformities in current density and temperature distribution, leading to reduced lifetime due to uneven heat distribution and mechanical stress, which conventional methods fail to adequately address.

Innovation Solution

A method to determine and optimize the spatial distribution of catalytic activity in electrochemical cell electrodes by measuring and adjusting thermal quantities to match a set-point temperature distribution, ensuring uniform temperature and extending cell lifetime.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Reliability

If conventional uniform catalytic activity distribution is used, then manufacturing is simple, but spatial nonuniformities in current density and temperature occur leading to reduced cell lifetime

Engineering Contradiction:
Improvecell lifetimeVSAvoidcatalytic activity distribution
Core Design Contradiction:
ReliabilityVSDevice complexity

Solution Approach 1:

The patent applies local quality by varying the catalytic activity distribution across different regions of the electrode. Specifically, the catalytic layer is designed with spatially varying catalyst concentration or activity to compensate for local temperature and current density nonuniformities. This allows each region to have optimized catalytic properties tailored to its specific operating conditions, thereby improving overall cell lifetime and performance uniformity.

Inventive Principle:
Principle #3Local quality

Solution Approach 2:

The patent implements parameter changes by modifying the catalytic activity parameter across the electrode surface. The catalytic activity is adjusted as a function of position to compensate for thermal and electrical nonuniformities. This involves changing catalyst loading, distribution, or composition parameters to achieve more uniform current density and temperature profiles throughout the cell.

Inventive Principle:
Principle #35Parameter changes

2Productivity

If catalytic activity is increased to improve reaction rate, then productivity increases, but temperature nonuniformities and hotspots worsen

Engineering Contradiction:
Improvereaction rateVSAvoidtemperature uniformity
Core Design Contradiction:
ProductivityVSTemperature

Solution Approach 1:

The patent applies local quality by designing regions with different catalytic activities to match local thermal conditions. Areas prone to overheating have reduced catalytic activity to lower heat generation, while cooler regions maintain higher activity to ensure sufficient reaction rate. This spatial differentiation of catalytic properties balances productivity with temperature uniformity.

Inventive Principle:
Principle #3Local quality

Solution Approach 2:

The patent implements feedback by using measured or simulated temperature and current density distributions to determine the optimal catalytic activity distribution. The catalytic design is based on feedback from thermal and electrical performance data, creating a compensated distribution that prevents hotspots while maintaining overall productivity.

Inventive Principle:
Principle #23Feedback

Applied Scientific Principles

This section explains which scientific principles are used to turn an abstract innovation direction into a practical engineering solution.

Function Achieved in This Case

The method ensures a uniform temperature distribution within electrochemical cells, preventing hotspots and mechanical stress, thereby enhancing the longevity and operational efficiency of the cells.

Implementation Method 1

a cooling circuit formed from a network of internal ducts that allow a heat-transfer fluid to flow and thus the heat produced locally during the reaction in the cell to be removed

Methodology Applied
Scientific EffectHeat transfer: Conduction (thermal)

Implementation Method 2

The active layer, which is located between the electrolytic membrane and the diffusion layer, is the site of the electrochemical reaction. It generally includes an electronic conductor (for example carbon), a protonic conductor (the electrolyte) and a catalyst, for example platinum particles.

Methodology Applied
Scientific EffectCatalysis: Catalysis

Implementation Method 3

The electrochemical reaction requires the presence of an ionic conductor between the two electrodes, namely the electrolyte

Methodology Applied
Scientific EffectIonic conduction: Conduction (electrical)

Implementation Method 4

The diffusion layer is located between the active layer and the corresponding bipolar plate. It is produced from a porous material allowing gaseous reactive species to diffuse as far as the active layer

Methodology Applied
Scientific EffectDiffusion: Diffusion

Data Source

PatentUS10181612B2Determination of a spatial distribution of the catalytic activity of an electrochemical-cell electrode
Publication Date: 2019.01.15 COMMISSARIAT A LENERGIE ATOMIQUE ET AUX ENERGIES ALTERNATIVES
  • US10181612B2 patent drawing
  • US10181612B2 patent drawing
  • US10181612B2 patent drawing

AI summary

A method is provided for determining a spatial distribution (Wcx,yf) of a parameter of interest (Wc) representative of a catalytic activity of an active layer of at least one electrode among two electrodes of an electrochemical cell, including steps of providing the cell, within which the parameter of interest (Wc) has an initial spatial distribution (Wcx,yi) of one or more values of catalytic load; defining a spatial distribution (Tx,yc) of a set-point temperature (Tc) within the cell in operation; measuring a spatial distribution (Dx,yr) of a first thermal quantity (Dr) within the cell in operation; estimating a spatial distribution (Wcx,ye) of a second thermal quantity (Qe) within the cell in operation, depending on the spatial distribution (Tx,yc) and on the measured spatial distribution (Dx,yr); and determining the spatial distribution (Wcx,yf) of the parameter of interest (Wc) depending on the estimated spatial distribution (Qx,ye) of the second thermal quantity (Qe).